US2300598A - Process of producing butene-2-diol-1, 4 and its substitution products - Google Patents

Description

pressure in a the presence num on carbon,

Patented Nov. 3, 1942 OFFICE PROCESS OF PRODUCING BUTENE-Z-DIOL- 1,4 AND ITS SUBSTITUTION PRODUCTS Willi Schmidt, Ludwigs and Kurt Heintz, Heidelgnors, by mesne assign- Richard Schnabel and hafen-on-the-Rhine, berg, Germany, assi ments, to General New York, N. Y., a

Aniline 8; Film Corporation, corporation 03 Delaware No Drawing. Application July 6, 1939, Serial No. 283,122. In Germany July 19, 1938 2 Claims.

The present invention relates to a process of producing butene-2-diol-L4 and its substitution products.

When subjecting butine-2-diol-L4 or its homologues to the action of hydrogen under increased of colloidal palladium, even at room temperature, practically only bu tane-dio1-l,4 is obtained. The other usual hydroge'natiom catalysts, as for example nickel, cobalt, copper, also yield mainly saturated diols when working in the liquid phase under the hydrogenation conditions usually in practice.

We have now found that butine-2-diol-1,4 and its substitution products of the formula:

v With all hydrogenation catalysts, which under normal conditions will fully hydrogenate the triple linkage of at least part of the butinediol an addition of carbon monoxide has proved suitable for this purpose. While for example nickel on carbon, finely divided cobalt, copper chromite catalysts, palladium on sillcic acid gel, platinum on carbon, without the addition of carbon monoxide yield practically only butanediol-1,4 at high hydrogen pressures and normal or moderately elevated temperatures, the addition of carbon monoxide, for example of from lto 20 per cent of the amount of hydrogen, has the effeet that good yields of butene-2-diol-l,4 are obtained with the same catalysts.

Similarly the activity of the catalyst may be reduced by applying it to carriers which are capable of reducing the activity thereof. Catalysts such as palladium on kieselguhr or cobalt, cobalt oxide, chromium oxide or copper oxide onbleaching earths thus yield butene-Z-diol-IA in good yields because the said weaklyacid carriers weaken the catalysts in their activity. On the contrary, for example with nickel or platibutane-diol-l,4 is obtained as above described.

increased hydrogen pres- The activity of the catalysts may also be weak ene d by adding to the reaction liquid substances which reduce the activity. This method has proved especially suitable when using precious metals as catalysts. Small amounts of phosphoric acid, secondary sodium phosphate, boric acid, potassium thiocyanide, sodium carbonate and piperidine may be enumerated as substances reducing the activity without limiting our invention to substances.

Two or more of the said measures which weaken the activity of the catalyst in favor of the formation of butene-2 -diol-1A may also be combined.

The temperatures suitable for the process are determined by the catalyst used. They usually lie below 200 C. A cobalt catalyst which would be very active under normal conditions may be used for-example satisfactorily even at ordinary temperature, while oxidic catalysts, as for example copper chromite or cobalt oxide on bleaching earths require a reaction temperature of about 150 0. Generally speaking temperatures of from 10 to 150 C. are favorable.

In order toobtain high yields per unit of space and time, it is preferable to employ pressures of atmospheres or more, as for example 250 atmospheres, although the hydrogenation also takes place at a useful speed at 50 or 10 atmospheres. The process may be carried out discontionuously or continuously.

The following examples will further illustrate how this invention may be carried out in practice but the invention is not restricted to these examples. The parts are by weight.

Example 1 I 200 parts of a crude 33 per cent aqueous butine-2-diol-l,4 solution in which 0.2 part of pothe use of these particular tassium thiocyanldeis dissolved are treated, after i the addition of 10 parts of finely divided cobalt suspended in 20 parts of water, in a high pressure autoclave at room temperature -while stir ring with hydrogen under a pressure of 100 atmospheres until the pressure remains constant. The catalyst is filtered of! from th reaction liquid and the water evaporated from the latter.

Practically pure butene-2-diol-L4 is thus obtained in a yield of 80 per cent of the theoretical yield. It boils at from 129 to 130 C. under; a pressure of 13 millimeters (mercury gauge). By working with the same catalyst without the addition of potassium thiocyanide in the presence of 5 atmospheres of carbonmonoxide, pure butene-2-diol-L4 is also obtained in a yield of 82 per cent of the theoretical yield.

if the activity of the cobalt catalyst be not 99.8 parts of carbon,

' bleaching earth, at 100 Example 2 10 parts of a copper chromite catalyst are added to 200 parts of a crude 50 per cent aqueous butine-2-diol-L4 solution and charged into a pressure vessel. After pressing in atmospheres of carbon monoxide the mixture is treated with hydrogen under a pressure of 120 atmospheres at 150 C. while stirring until hydrogen is no longer absorbed. The catalyst may be used repeatedly. After evaporating the water, the residue yields a completely pure butene-2'-diol-l,4 (boiling point 130 C. at 13 millimeters) in a good yield.

' With a copper chromite catalyst which has not been weakened, in its activity there is obtained under the same conditions a mixture of butene- 2-diol-l,4 and mainly butane-diol-1,4..

Example 3 0.3 part of secondary sodium phosphate is dissolved in 200 parts of a 20 per cent aqueous crude butine-2-diol l,4 solution. After adding parts of a catalyst containing 0.2 parts of platinum on it is hydrogenated in a stirring autoclave at 150 C. and a hydrogen pressure of 150 atmospheres until the absorption of hydrogen ceases. Practically pure butene-Z- dial-1,4 is obtained in a yield of 80 per cent of the theoretical yield.-

If 0.15 parts of boric acid or. 3 parts of piperidine be added to the butine-2-diol-1,4 solution as the weakening addition for the catalyst instead of 0.3 part of secondary sodium phosphate, butene-2-diol-1,4 is also obtained in a good yield.

An addition of 5 atmospheres of carbon monoxide also effects the formation of a very pure butene-2-diol-.1,4 in a yield of about 90 per cent of the theoretical yield. If the hydro-' genation be carried out without weakening the activity of the catalyst, pure butane-diol-1,4 is obtained. A

Butene-2-diol-1,4 is obtained in 70 per "tent of the theoretical yield when working in the following manner: 100 parts of an aqueous 30 per cent solution of butine-2-diol-1,4 are charged into a pressure-tight vessel. After addin 5parts of the platinum catalyst referred to above, carbon monoxide of 2 atmospheres pressure is pressed in, and then hydrogen of 10 atmospheres pressure is introduced at 190 C. until it is no longer absorbed.

Example 4 200 parts of a 33 per cent aqueous butine-2- diol1,4 solution are hydrogenated in the usual way in the presence of 10 parts of a catalyst containing parts'of c balt on 80 parts of C. under a hydrogen pressure of 120 atmospheres until hydrogen is no longer absorbed. Avery pure butene-2-diol- 1,4 is obtained in a yield of '75 per cent of the theoretical yield. 7

Metal oxides which are applied to bleaching earths, such as cobalt oxide, or mixtures of chromium oxide and copper oxide, also hydrogenate butine-2-diol-1,4 in good yields to pure butene-2-diol-l,4.

Example 5 I 1 liter of an about 33 per cent crude solution of 'butine-2-diol-l,4 (obtained from formaldehyde and acetylene) is first shaken with 20 grams of animal carbon and then filtered. The whole is then treated in a pressure vessel, after adding 50 grams of a'catalyst obtained by applying 0.2 gram of palladium to 1 liter of pure kieselguhr, with hydrogen under a pressure of about 20 atmospheres and at 100 C. until hydrogen is no longer absorbed, which is the case after from about 10 to 20 hours. The filtered catalyst can be used repeatedly. After careful evaporation of the water,'butene-2-diol-1,4 having a boiling point of from 107 to 110 C. at a pressure of from 1.0 to 1.4 millimeters is obtained in a very good yield.

For the purpose of comparison, the following is a description of the hydrogenation of butine- 2-diol-l,4 with colloidal palladium.

A solution of 4.018 grams of pure butine-2- diol-1,4 in 35 cubic centimeters of methanol is ing to 2098.5 cubic centimeters of hydrogen ,un-

. der. normal conditions,

while for the absorption of 2 molecular proportions of hydrogen, 2045 cubic centimeters is the calculated amount.

Thus 2 molecular proportions of hydrogen have been absorbed, the butine-2-diol-1,4 being converted into butane-diol-1,4.

Whatwe claim is: v

1. A process for the production of butene-2- diol-l,4,which consists in treating in the liquid phase with a mixture of hydrogen and carbon monoxide in which hydrogen preponderates by mols under superatmospheric pressure butine-2- diol-1,4 in the presence of a hydrogenation catalyst until hydrogen is no longer absorbed.

2. A process for the production of butene-2- diol-1,4 and its substitution products which consists in treating in the liquid phase with hydrogen under superatmospheric pressure a member of the group consisting of butine-2-diol-l,4 and butine-2-diol-1,4 substituted in at least one of the 1- and 4-positions by a hydrocarbon radical in the presence of a hydrogenation catalyst and in the presence of carbon monoxide until hydrogen is no'lon'ger absorbed.

RICHARD SCHNABEL. WILLI SCHMIDT. KURT HEINTZ.